DE58906173D1 - Process for the separation of arsenic from waste water. - Google Patents

Process for the separation of arsenic from waste water.

Info

Publication number
DE58906173D1
DE58906173D1 DE89105712T DE58906173T DE58906173D1 DE 58906173 D1 DE58906173 D1 DE 58906173D1 DE 89105712 T DE89105712 T DE 89105712T DE 58906173 T DE58906173 T DE 58906173T DE 58906173 D1 DE58906173 D1 DE 58906173D1
Authority
DE
Germany
Prior art keywords
removal
arsenic
waste water
contacting
activated carbon
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
DE89105712T
Other languages
German (de)
Inventor
Georg Dipl Ing Schuster
Hans Dipl Ing Kaestle
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Walhalla Kalk Entwickl and Vertriebs GmbH
Original Assignee
Walhalla Kalk Entwickl and Vertriebs GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Walhalla Kalk Entwickl and Vertriebs GmbH filed Critical Walhalla Kalk Entwickl and Vertriebs GmbH
Application granted granted Critical
Publication of DE58906173D1 publication Critical patent/DE58906173D1/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B30/00—Obtaining antimony, arsenic or bismuth
    • C22B30/04—Obtaining arsenic
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • C02F2001/422—Treatment of water, waste water, or sewage by ion-exchange using anionic exchangers
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/10—Inorganic compounds
    • C02F2101/103—Arsenic compounds
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/12—Nature of the water, waste water, sewage or sludge to be treated from the silicate or ceramic industries, e.g. waste waters from cement or glass factories
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S210/00—Liquid purification or separation
    • Y10S210/902—Materials removed
    • Y10S210/911—Cumulative poison

Abstract

The process for removal of arsenic from waste waters is characterised by (A1) precipitation of the arsenic in the form of sparingly soluble calcium magnesium arsenates by addition of calcium compounds and magnesium compounds to the waste water at pH 2 to 12 and (A2) removal of the calcium magnesium arsenates and/or (B1) contacting the waste water with an ion exchanger at pH 2 to 12 and optionally (B2) regeneration of the ion exchanger after reaching the limit of the capacity and/or (C1) adsorptive removal of the aresenic by contacting the waste water with activated carbon at pH 2 to 11 and (C2) removal of the charged activated carbon alone or together with precipitation products. <??>The process permits removal of arsenic, in particular even in the case of waste waters that are difficult to treat and contain heavy metals such as lead, and also sulphate, to residual contents < 0.3 mg AS/l.
DE89105712T 1989-03-31 1989-03-31 Process for the separation of arsenic from waste water. Expired - Fee Related DE58906173D1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP19890105712 EP0389661B1 (en) 1989-03-31 1989-03-31 Process for removing arsenic from waste waters

Publications (1)

Publication Number Publication Date
DE58906173D1 true DE58906173D1 (en) 1993-12-16

Family

ID=8201158

Family Applications (1)

Application Number Title Priority Date Filing Date
DE89105712T Expired - Fee Related DE58906173D1 (en) 1989-03-31 1989-03-31 Process for the separation of arsenic from waste water.

Country Status (7)

Country Link
US (1) US5114592A (en)
EP (1) EP0389661B1 (en)
JP (1) JPH02293089A (en)
AT (1) ATE97116T1 (en)
CA (1) CA2012472C (en)
DE (1) DE58906173D1 (en)
ES (1) ES2048224T3 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113227418A (en) * 2018-12-24 2021-08-06 环保金属有限公司 Method for obtaining scorodite with high arsenic content from acidic solution with high sulfuric acid content

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DE3926586A1 (en) * 1989-08-11 1991-02-14 Haecker Maschinen Gmbh Ing Cleaning waste water from glass industry - using type I or II anion exchangers to remove arsenic and antimony fluoride complex ions
DE3941989C2 (en) * 1989-08-11 1995-09-21 Haecker Maschinen Gmbh Ing Process for cleaning acidic, etc. Waste water from the glass industry containing arsenic
US5262063A (en) * 1992-05-14 1993-11-16 Elf Atochem North America, Inc. Multiple-stage precipitation process for heavy metals in aqueous solution
US5348662A (en) * 1992-05-14 1994-09-20 Elf Atochem North America, Inc. Process for removing heavy metals from aqueous solutions
DE69307328T2 (en) * 1992-09-17 1997-04-24 Allied Signal Inc METHOD FOR CONVERTING HEXAFLUORIC ACID OR ITS SALTS IN A WATER-INSOLUBLE ARSENATE SALT THAT CAN THEN BE DAMAGED
US5378366A (en) * 1993-04-22 1995-01-03 Elf Atochem North America, Inc. Hot lime precipitation of arsenic from wastewater or groundwater
US5320756A (en) * 1993-06-29 1994-06-14 Church & Dwight Co., Inc. Method of treating aqueous alkaline effluents derived from cleaning electronic circuit assemblies
US5320758A (en) * 1993-06-29 1994-06-14 Church & Dwight Co., Inc. Method of recycling amine saponifiers used in cleaning electronic circuit boards
US5358643A (en) * 1994-02-08 1994-10-25 Mcclintock William W Treatment method for removing arsenic from arsenic contaminated water
US5451414A (en) * 1994-03-15 1995-09-19 Heritage Environmental Services, Inc. Micronutrient supplement
DE19500057C1 (en) * 1995-01-03 1996-02-29 Starck H C Gmbh Co Kg Environmentally friendly prodn. of pure tungstate and molybdate soln.
US6387276B1 (en) * 1997-06-19 2002-05-14 The University Of Connecticut Immobilization of inorganic arsenic species using iron
US5972073A (en) * 1997-10-02 1999-10-26 The University Of Dayton Recovery of the components of group III-V material aqueous wastes
US6126719A (en) * 1998-01-21 2000-10-03 The University Of Dayton Recovery of group III element component from group III-V waste materials
US6254312B1 (en) * 1998-06-18 2001-07-03 Rmt, Inc. Stabilization of arsenic-contaminated materials
US6843617B2 (en) * 1998-06-18 2005-01-18 Rmt, Inc. Stabilization of toxic metals in a waste matrix and pore water
FR2784295B1 (en) * 1998-10-09 2002-02-08 Instrumentation Scient Et Ind PROCESSES FOR THE PREPARATION OF AN ALGAL EXTRACT ANRICHED IN IODINE AND A SKIN PATCH WITH GRADUAL RELEASE OF IODINE AND THE CORRESPONDING PRODUCTS
US6265438B1 (en) 1998-12-03 2001-07-24 Heritage Technologies, Llc Vitamin compatible micronutrient supplement
US6461535B1 (en) 1999-12-03 2002-10-08 Pan American Health Organization Composition for arsenic removal from ground water
JP4077143B2 (en) * 2000-07-31 2008-04-16 日本特殊陶業株式会社 Chromate drainage treatment method
US20050247635A1 (en) * 2001-08-27 2005-11-10 Vo Toan P Adsorbents for removing heavy metal cations and methods for producing and using these adsorbents
US7429551B2 (en) * 2001-08-27 2008-09-30 Calgon Carbon Corporation Adsorbents for removing heavy metals
US7429330B2 (en) * 2001-08-27 2008-09-30 Calgon Carbon Corporation Method for removing contaminants from fluid streams
US20050093189A1 (en) * 2001-08-27 2005-05-05 Vo Toan P. Adsorbents for removing heavy metals and methods for producing and using the same
US6914034B2 (en) 2001-08-27 2005-07-05 Calgon Carbon Corporation Adsorbents for removing heavy metals and methods for producing and using the same
US7247242B1 (en) * 2001-10-10 2007-07-24 Sandia Corporation Arsenic removal from water
US6821434B1 (en) * 2001-10-10 2004-11-23 Sandia Corporation System for removal of arsenic from water
US20040076668A1 (en) * 2002-07-03 2004-04-22 Pfizer Inc. Controlled-release pharmaceutical formulations
TW559617B (en) * 2003-05-07 2003-11-01 Ind Tech Res Inst Method for removing arsenic from water
AU2004274472B2 (en) * 2003-09-19 2010-07-08 University Of Wyoming System and method for removing arsenite and arsenate from water
EP1727618A4 (en) * 2004-01-21 2011-03-09 Sengupta Arup K Method of manufacture and use of hybrid anion exchanger for selective removal of contaminating ligands from fluids
DE602005025268D1 (en) * 2004-02-24 2011-01-27 Rohm & Haas Method of removing arsenic from water
JP4598415B2 (en) * 2004-02-27 2010-12-15 オルガノ株式会社 Organic arsenic compound processing method
CA2579031C (en) * 2006-03-03 2011-03-29 Rohm And Haas Company Method for producing an arsenic-selective resin
ITMI20062524A1 (en) * 2006-12-28 2008-06-29 Itea Spa PROCESS FOR PURIFICATION OF COMBUSTION FUMES
DE102007009362A1 (en) * 2007-02-23 2008-08-28 Mion Tec Gmbh Process for removing arsenic from aqueous solutions
JP5137232B2 (en) * 2007-04-02 2013-02-06 Ｄｏｗａメタルマイン株式会社 Method for producing porous iron oxide and method for treating water to be treated
FI122512B (en) * 2011-03-09 2012-02-29 Outotec Oyj Process for the preparation of a sparingly soluble calcium arsenic compound
CN105347544B (en) * 2015-10-31 2016-07-13 江西铜业股份有限公司 A kind of method of precipitate and separate arsenic from acid water
CN111170510B (en) * 2020-01-20 2022-03-29 宁波弗镁瑞环保科技有限公司 Method for treating arsenic-containing wastewater and solidifying arsenic
CN112063858A (en) * 2020-09-08 2020-12-11 龙岩市宇恒环保科技有限公司 Process for producing qualified arsenic oxide from arsenic-containing material by full-wet method
CN114836635B (en) * 2022-03-25 2023-05-16 中南大学 Method for preparing high-purity metal arsenic by nonferrous smelting arsenic-containing solid waste short process
CN114892027B (en) * 2022-07-15 2022-10-28 长沙华时捷环保科技发展股份有限公司 Method for directly separating arsenic from arsenic-containing solution

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US3414512A (en) * 1966-11-30 1968-12-03 United States Steel Corp Method of flocculating solids
JPS50138650A (en) * 1974-04-22 1975-11-05
JPS516885A (en) * 1974-07-09 1976-01-20 Osaka Soda Co Ltd Ekitaichuno jukinzokujokyohoho
JPS6036831B2 (en) * 1978-07-05 1985-08-22 三菱レイヨン株式会社 Treatment method for water containing arsenic and silica
CA1139466A (en) * 1980-08-22 1983-01-11 Donald R. Weir Removal of arsenic from aqueous solutions
US4341636A (en) * 1980-09-26 1982-07-27 General Electric Company Treatment of wastewater
SE452307B (en) * 1983-09-12 1987-11-23 Boliden Ab PROCEDURE FOR PURIFICATION OF POLLUTANEOUS WATER SOLUTIONS CONTAINING ARSENIC AND / OR PHOSPHORUS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113227418A (en) * 2018-12-24 2021-08-06 环保金属有限公司 Method for obtaining scorodite with high arsenic content from acidic solution with high sulfuric acid content

Also Published As

Publication number Publication date
US5114592A (en) 1992-05-19
ES2048224T3 (en) 1994-03-16
ATE97116T1 (en) 1993-11-15
EP0389661B1 (en) 1993-11-10
JPH02293089A (en) 1990-12-04
CA2012472A1 (en) 1990-09-30
CA2012472C (en) 2000-03-14
EP0389661A1 (en) 1990-10-03

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Legal Events

Date Code Title Description
8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee